BACKGROUND
1. Field
[0001] The present disclosure relates to heat exchangers, more specifically to headers for
heat exchangers.
2. Description of Related Art
[0002] Heat exchangers are central to the functionality of numerous systems (e.g., in engines
and environmental controls systems (ECS), e.g. for aircraft). On engines, heat exchangers
are used for a variety of oil and air cooling applications. Heat exchangers are central
to the operation of environmental control systems (air cycles) as well as other cooling
systems. All of these applications continually require increases in heat transfer
performance, reductions in pressure loss, and reductions in size and weight.
[0003] Current heat exchanger offerings are dominated by plate fin construction, with tube
shell and plate-type heat exchangers having niche applications. Traditional plate
fin construction imposes multiple design constraints that inhibit performance, increase
size and weight, suffer structural reliability issues, are unable to meet future high
temperature applications, and limit system integration opportunities.
[0004] Certain heat exchangers require transitioning from pipe flow to a layered arrangement
in a heat exchanger core. These types of systems require special headers and can significantly
impact the overall performance.
[0005] Such conventional methods and systems have generally been considered satisfactory
for their intended purpose. However, there is still a need in the art for headers
for heat exchangers. The present disclosure provides a solution for this need.
SUMMARY
[0006] A heat exchanger header includes a plurality of first flow channels and second flow
channels, each flow channel including a fluid circuit opening for fluid communication
with a fluid circuit of a heat source and a core opening for communication with a
heat exchanger core, wherein at least the first flow channels include a lobe section
defining a non-uniform cross-sectional flow area that changes along a flow direction.
The non-uniform cross-sectional flow area can change in two dimensions along at least
a portion of the lobe section, for example.
[0007] The non-uniform cross-sectional area can change non-linearly. In certain embodiments,
the lobe section can have a bulb shape. In certain embodiments, at least the first
flow channels can include a uniform section including a uniform cross-sectional area
or a linearly changing cross-sectional flow area.
[0008] The lobe section can be disposed between the fluid circuit opening and the uniform
section. The uniform section can be disposed between the lobe section and the core
opening.
[0009] The lobe section can expand in flow area from the fluid circuit opening to a maximum
flow area, wherein the lobe section then can reduce in flow area from the maximum
flow area to the uniform section flow area.
[0010] The first flow channel can include a constantly expanding flow area from the flow
circuit opening to the core opening in a first dimension and an expanding flow area
at the lobe section in an orthogonal direction which then reduces from the lobe section
toward the core opening.
[0011] The first flow channels can be hot flow channels and the second flow channels can
be cold flow channels. Flow can be arranged to be counter-flow between the first flow
channels and the second flow channels, however, parallel flow is also contemplated
herein.
[0012] A heat exchanger, includes a core defining a plurality of core openings and a header
as described above connected to the core.
[0013] These and other features of the systems and methods of the subject disclosure will
become more readily apparent to those skilled in the art from the following detailed
description taken in conjunction with the drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0014] So that those skilled in the art to which the subject disclosure appertains will
readily understand how to make and use the devices and methods of the subject disclosure
without undue experimentation, embodiments thereof will be described in detail herein
below with reference to certain figures, wherein:
Fig. 1A is a rear view of an embodiment of a heat exchanger in accordance with this
disclosure;
Fig. 1B is a top plan view of the embodiment of a heat exchanger of Fig. 1A;
Fig. 1C is a front view of the embodiment of a heat exchanger of Fig. 1A;
Fig. 1D is a side view of the embodiment of a heat exchanger of Fig. 1 A;
Fig. 1E is a schematic indicating the orientation of the of the embodiment of a heat
exchanger of Figs. 1A-1D;
Fig. 2A is a rear view of an embodiment of a heat exchanger in accordance with this
disclosure;
Fig. 2B is a top plan view of the embodiment of a heat exchanger of Fig. 2A;
Fig. 3A is a rear view of an embodiment of a heat exchanger in accordance with this
disclosure;
Fig. 3B is a top plan view of the embodiment of a heat exchanger of Fig. 3A;
Fig. 4A is a rear view of an embodiment of a heat exchanger in accordance with this
disclosure;
Fig. 4B is a top plan view of the embodiment of a heat exchanger of Fig. 4A;
Fig. 4C is a front view of the embodiment of a heat exchanger of Fig. 4A;
Fig. 4D is a side view of the embodiment of a heat exchanger of Fig. 4A; and
Fig. 4E is a schematic indicating the orientation of the of the embodiment of a heat
exchanger of Figs. 4A-4D.
DETAILED DESCRIPTION
[0015] Reference will now be made to the drawings wherein like reference numerals identify
similar structural features or aspects of the subject disclosure. For purposes of
explanation and illustration, and not limitation, an illustrative view of an embodiment
of a heat exchanger in accordance with the disclosure is shown in Fig. 1A and is designated
generally by reference character 100. Other embodiments and/or aspects of this disclosure
are shown in Figs. 1B-4E. The systems and methods described herein can be used to
improve heat exchanger efficiency, for example.
[0016] Referring to Figs. 1A-1E, a heat exchanger 100 includes a header 101 that has a plurality
of first flow channels 103 and second flow channels 105. Each flow channel 103, 105
includes a fluid circuit opening 106, 107 (e.g., as shown in Fig. 1B) for fluid communication
with a fluid circuit (not shown) of a heat source (e.g., an aircraft system, not shown)
and a core opening 109 for communication with a heat exchanger core 111. For example,
fluid circuit opening 107 can be a hot flow opening and fluid circuit opening 106
can be a cold flow opening.
[0017] At least the first flow channels 103 can include a lobe section 113 (e.g., as shown
in Fig. 1A) defining a non-uniform cross-sectional flow area that changes along a
flow direction. The non-uniform cross-sectional flow area can change in at least two
dimensions (e.g., in the x and y axes as shown) along at least a portion of the lobe
section 113, for example. In certain embodiments, the lobe section 113 can become
wider in the x-axis from the fluid circuit opening 107 toward the core 111 and can
become wider in the y-axis and/or z-axis simultaneously.
[0018] As shown, the non-uniform cross-sectional area can change non-linearly. In certain
embodiments, the lobe section 113 can have a bulb shape as shown. In certain embodiments,
at least the first flow channels 103 can include a uniform section 115 including a
uniform cross-sectional area or a linearly changing cross-sectional flow area.
[0019] The lobe section 113 can be disposed between the fluid circuit opening 107 and the
uniform section 115. Similarly, the uniform section 115 can be disposed between the
lobe section 113 and the core opening 111. A transition can exist between the non-uniform
flow area and a uniform flow area. Certain embodiments do not include a uniform section
115.
[0020] As shown, the lobe section 113 can expand in flow area from the fluid circuit opening
107 to a maximum flow area. The lobe section 113 then can reduce in flow area from
the maximum flow area to the uniform section 115 flow area.
[0021] Restated, the first flow channel 103 can include a constantly expanding flow area
from the flow circuit opening 107 to the core opening 109 in a first dimension (e.g.,
the y-axis and/or the z-axis) and an expanding flow area at the lobe section 113 in
an orthogonal direction (e.g., in the x-axis) which then reduces from the lobe section
113 toward the core opening 109.
[0022] In certain embodiments, total flow area from flow circuit opening 107 of the first
channels 103 is no more than total flow at the point of entering core 111 to prevent
flow diffusion and then constriction again. In this regard, the lobe section 113 flow
area can be sized to provide an expansion, e.g., in the x-axis, until the expansion
in the z-axis and/or y-axis is at a maximum width in the x-axis is reached, at which
point a reduction in the width in the x-axis can be had since the expansion in the
z-axis and/or y-axis is sufficient to maintain a constant total flow area, a constantly
expanding total flow area, or a constantly reducing total flow area from the flow
circuit opening 107 to the core opening 109.
[0023] The first flow channels 103 can be hot flow channels and the second flow channels
105 can be cold flow channels, however, it is contemplated the channels 103, 105 can
be used for hot or cold flow. Flow can be arranged to be counter-flow between the
first flow channels 103 and the second flow channels 105, however, parallel flow is
also contemplated herein.
[0024] As shown in Fig. 1B, the first flow channels 103 can include a curved shape in the
y-z plane (e.g., to form a U-shape). As shown, the flow circuit openings 107 can both
be configured to face down. Referring to Figs. 2A and 2B, certain embodiments of a
heat exchanger 200 can include first flow channels 107 that have flow circuit openings
107 in opposite or otherwise different directions (e.g., to form an S-shape).
[0025] Referring to Figs. 3A and 3B, another embodiment of a heat exchanger 300 is shown.
As shown, certain embodiments can include a header 301 that is wider (e.g., in the
x-axis) than the core 111 but reduces down to the core 111 in total dimension, for
example. The expansion could be symmetric as shown or could skew to one side or the
other. Any suitable relative dimensions of the header 301 as compared to the core
111 are contemplated herein.
[0026] A total header width/height can be taller than the core 111 to mitigate pressure
drop (e.g., as shown in Fig. 3). Embodiments of headers 101 are arranged in layers
of hot and cold flow and contract or expand as in a scoop or nozzle, for example.
By using taller channels away from the core, the hot-side flow velocities and pressure
drops can be reduced. Increasing the height of the hot layers reduces the height of
the cold-side layers if the total height of the headers is kept constant. By allowing
the width of the header to vary, a similar increase in hot-side height can be used
without significantly reducing cold-side flow area.
[0027] Also, as shown in the embodiment of Fig. 2B, the width of the second flow channels
105 can be increased (e.g., in the z-axis) by following the inside curve of the first
flow channels 103, thereby mitigating the loss in flow area on the cold-side due to
the increased height of the hot-side layers. In this case, at least part of the cold-side
flow can follow a curve rather having a straight path though the device.
[0028] Referring to Fig. 4A-4E, another embodiment of a heat exchanger 400 is shown. As
shown, the lobe section 113 can extend from the channels 103 such that the channels
103, 105 above the lobe section 113 are plate shaped (e.g., with a constant width
in the x-axis). Any other suitable location and shape for the lobe sections 113 are
contemplated herein.
[0029] The methods and systems of the present disclosure, as described above and shown in
the drawings, provide for heat exchanger headers with superior properties. While the
apparatus and methods of the subject disclosure have been shown and described with
reference to embodiments, those skilled in the art will readily appreciate that changes
and/or modifications may be made thereto without departing from the scope of the present
invention, defined by the claims.
1. A heat exchanger header, comprising:
a plurality of first flow channels (103) and second flow channels (105), each flow
channel including a fluid circuit opening (106, 107) for fluid communication with
a fluid circuit of a heat source and a core opening (109) for communication with a
heat exchanger core (111), wherein at least the first flow channels include a lobe
section (113) defining a non-uniform cross-sectional flow area that changes along
a flow direction.
2. The header of claim 1, wherein the non-uniform cross-sectional flow area changes in
two dimensions along at least a portion of the lobe section.
3. The header of claim 2, wherein the non-uniform cross-sectional area changes non-linearly.
4. The header of claim 3, wherein the lobe section has a bulb shape.
5. The header of any preceding claim, wherein at least the first flow channels include
a uniform section including a uniform cross-sectional area or a linearly changing
cross-sectional flow area.
6. The header of claim 5, wherein the lobe section is disposed between the fluid circuit
opening and the uniform section.
7. The header of claim 6, wherein the uniform section is disposed between the lobe section
and the core opening.
8. The header of claim 5, wherein the lobe section expands in flow area from the fluid
circuit opening to a maximum flow area, wherein the lobe section reduces in flow area
from the maximum flow area to the uniform section flow area.
9. The header of claim 5, wherein the first flow channels (103) include a constantly
expanding flow area from the flow circuit opening to the core opening in a first dimension
and an expanding flow area at the lobe section in an orthogonal direction which then
reduces from the lobe section toward the core opening.
10. The header of any preceding claim, wherein the first flow channels (103) are hot flow
channels and the second flow channels (105) are cold flow channels.
11. A heat exchanger, comprising:
a core (111) defining a plurality of core openings (109); and
a header (101) connected to the core, the header including a plurality of first flow
channels (103) and second flow channels (105), each flow channel including a fluid
circuit opening (106, 107) for fluid communication with a fluid circuit of a heat
source and a core opening (109) for communication with a heat exchanger core, wherein
at least the first flow channels include a lobe section defining a non-uniform cross-sectional
flow area that changes along a flow direction.
12. The heat exchanger of claim 11, wherein the non-uniform cross-sectional flow area
changes in two dimensions along at least a portion of the lobe section.
13. The heat exchanger of claim 12, wherein the non-uniform cross-sectional area changes
non-linearly.
14. The heat exchanger of claim 13, wherein the lobe section has a bulb shape.
15. The heat exchanger of any of claims 11 to 14, wherein at least the first flow channels
include a uniform section including a uniform cross-sectional area or a linearly changing
cross-sectional flow area.